US4897357A - (S) α-cyano-3-phenoxy-benzyl acetate - Google Patents
(S) α-cyano-3-phenoxy-benzyl acetate Download PDFInfo
- Publication number
- US4897357A US4897357A US07/226,824 US22682488A US4897357A US 4897357 A US4897357 A US 4897357A US 22682488 A US22682488 A US 22682488A US 4897357 A US4897357 A US 4897357A
- Authority
- US
- United States
- Prior art keywords
- cyano
- phenoxy
- benzyl acetate
- reaction
- benzyl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C255/00—Carboxylic acid nitriles
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/8215—Microorganisms
- Y10S435/911—Microorganisms using fungi
- Y10S435/921—Candida
Definitions
- This invention relates to optically active (S) ⁇ -cyano-3-phenoxy-benzyl acetate and to a method for biologically preparing the same. More particularly, it relates to (S) ⁇ -cyano-3-phenoxy-benzyl acetate and to a method for preparing the same characterized by allowing a racemic mixture of (R,S) ⁇ -cyano-3-phenoxy-benzyl acetate to react with a lipase originated from a microorganism which is capable of asymmetrically hydrolyzing the ester of the (R) alcohol in the racemic mixture to give (R) ⁇ -cyano-3-phenoxy-benzyl alcohol and (S) ⁇ -cyano-3-phenoxy-benzyl acetate.
- European Patent Application No. 84300024.1 discloses a method for biologically preparing optically active (S) o-cyano-3-phenoxy-benzyl alcohol, which is the alcohol moiety of certain pyrethroids, by reacting an ester of racemic (R,S) ⁇ -cyano-3-phenoxy-benzyl alcohol with an esterase wherein the ester of (S) ⁇ -cyano-3-phenoxy-benzyl alcohol is predominantly hydrolyzed thereby permitting optical resolution of the (S)-isomer alcohol from the ester of its antipode.
- R,S racemic
- S ⁇ -cyano-3-phenoxy-benzyl alcohol
- an esterase wherein the ester of (S) ⁇ -cyano-3-phenoxy-benzyl alcohol is predominantly hydrolyzed thereby permitting optical resolution of the (S)-isomer alcohol from the ester of its antipode.
- the process of the invention for the preparation of (S) ⁇ -cyano-3-phenoxy-benzyl acetate comprises reacting (R,S) ⁇ -cyano-3-phenoxy-benzyl acetate with a lipase originating from a microorganism and capable of asymmetrically hydrolyzing the (R) ⁇ -cyano-3-phenoxy-benzyl acetate ester to give optically active (R) ⁇ -cyano-3-phenoxy-benzyl alcohol and (S) ⁇ -cyano-3-phenoxybenzyl acetate.
- the ester of the (S) alcohol and the (R) alcohol are then separated from the reaction mixture and thereafter the ester of the (S) alcohol is separated and recovered from the (R) alcohol.
- the lipases employable in the present invention are those capable of asymmetrically hydrolyzing the ester of (R) ⁇ -cyano-3-phenoxy-benzyl alcohol and they are originated from microorganisms.
- an employable lipase is a carboxylic acid hydrolase originated from the genus Candida, and particularly, the strain Candida cylindricae, also known as Candida rugosa.
- the enzyme is commercially available from the Sigma Chemical Company, Post Office Box 14508, St. Louis, Mo. 63178.
- the asymmetric hydrolysis of the (R) ester is carried out by stirring or shaking a racemic mixture of (R,S) ⁇ -cyano-3-phenoxy-benzyl acetate and a lipase-containing liquor, such as a cultured liquor of such microorganism, its filtrate, lipase extracted liquor and its concentrate, a suspension of microorganism cells or aqueous solution containing crude or purified lipase preparation.
- a lipase-containing liquor such as a cultured liquor of such microorganism, its filtrate, lipase extracted liquor and its concentrate, a suspension of microorganism cells or aqueous solution containing crude or purified lipase preparation.
- the process can be carried out at ambient conditions although it is preferred to carry out the reaction at elevated temperatures varying from about 40° C. to 50° C. since at elevated temperatures the reaction rates are much faster.
- the period of time for the reaction is typically from about 10 to 40 hours. However, the reaction time can be shortened by increasing the reaction temperature or by increasing the concentration of enzyme.
- the hydrolysis reaction should be conducted at a pH no higher than pH 8. Furthermore, a pH which is too low will cause deactivation of the enzyme.
- the reaction is preferably conducted in the range of pH 4 to pH 8, most preferably pH 5 to pH 6.
- a buffer solution may be used to prevent the lowering of the pH value due to the formation of organic acid during the course of hydrolysis. Either an inorganic or organic salt buffer can be used as the buffer solution.
- the (S) ⁇ -cyano-3-phenoxy-benzyl acetate ester and the (R) alcohol are separated from the reaction mixture by solvent extraction, liquid phase separation by standing, column chromatography or other conventional separation techniques.
- the ester is then separated from the alcohol by chromatography, preferably chromatography over silica gel.
- (S) ⁇ -cyano-3-phenoxy-benzyl acetate is useful as an intermediate for the production of synthetic pyrethroids such as fenvalerate, cypermethryn, and decamethrin and is deemed to possess insecticidal, herbicidal and bactericidal activities of its own.
- the reaction mixture was then extracted with toluene.
- the toluene extract was concentrated by vacuum distillation to yield a yellow oil.
- the yellow oil was mixed with 123 milliliters of 0.2M concentration of a sodium acetate buffer solution (pH 5.0) and 2.25grams of Candida cylindricae lipase.
- the mixture was incubated with stirring at 25° C. for 18 hours and extracted with toluene as described above to yield a yellow oil containing 37% ⁇ -cyano-3-phenoxy-benzyl acetate, 45% ⁇ -cyano-3-phenoxy-benzyl alcohol and 15% m-phenoxybenzaldehyde as determined by gas chromatography.
- the (S) ⁇ -cyano-3-phenoxy-benzyl acetate was purified by column chromatography.
- the oil was placed on a column containing Kieselgel 40 (60-230 mesh) and eluted with a mixture of heptane and ethyl acetate in a ratio of 85 parts heptane to 15 parts ethyl acetate.
- the fractions containing only (S) ⁇ -cyano-3-phenoxy-benzyl acetate were combined and concentrated by vacuum distillation to yield a yellow oil.
- the oil (116 milligrams) was combined with enough benzene to bring the total volume to 1.16 milliliters.
- the benzene solution was analyzed on a Perkin-Elmer Model 241 Polarimeter and yielded a positive rotation of +17.1° at 20° C.
- the ⁇ -cyano-3-phenoxy-benzyl acetate fraction was analyzed on NMR using a chiral shift reagent [Eu(C 12 H 14 F 3 O 2 )3]. Analysis showed that the ⁇ -cyano-3-phenoxy-benzyl acetate consisted of a mixture containing 75-85% (S) ⁇ -cyano-3-phenoxy-benzyl acetate and 15-25% (R) ⁇ -cyano-3-phenoxy-benzyl acetate.
- the ⁇ -cyano-3-phenoxy-benzyl alcohol fraction was analyzed by high performance liquid chromatography as described in Example 1.
- the ⁇ -cyano-3-phenoxy-benzyl alcohol fraction consisted exclusively of (R) ⁇ -cyano-3-phenoxy-benzyl alcohol.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
(S) α-cyano-3-phenoxy-benzyl acetate having the formula: ##STR1## and a novel process for its preparation.
Description
This application is a division of application Ser. No. 815,207, filed Dec. 31, 1985, now U.S. Pat. No. 4,827,013.
This invention relates to optically active (S) α-cyano-3-phenoxy-benzyl acetate and to a method for biologically preparing the same. More particularly, it relates to (S) α-cyano-3-phenoxy-benzyl acetate and to a method for preparing the same characterized by allowing a racemic mixture of (R,S) α-cyano-3-phenoxy-benzyl acetate to react with a lipase originated from a microorganism which is capable of asymmetrically hydrolyzing the ester of the (R) alcohol in the racemic mixture to give (R) α-cyano-3-phenoxy-benzyl alcohol and (S) α-cyano-3-phenoxy-benzyl acetate.
(R,S) α-cyano-3-phenoxy-benzyl acetate, which is a racemic mixture, is known.
European Patent Application No. 84300024.1 discloses a method for biologically preparing optically active (S) o-cyano-3-phenoxy-benzyl alcohol, which is the alcohol moiety of certain pyrethroids, by reacting an ester of racemic (R,S) α-cyano-3-phenoxy-benzyl alcohol with an esterase wherein the ester of (S) α-cyano-3-phenoxy-benzyl alcohol is predominantly hydrolyzed thereby permitting optical resolution of the (S)-isomer alcohol from the ester of its antipode. Thus, there is provided in the art a biological method capable of producing (R) α-cyano-3-phenoxy-benzyl acetate. Until Applicants' invention, however, there has existed no known method for producing the (S)-isomer of α-cyano-3-phenoxy-benzyl acetate insofar as Applicants are aware.
Thus, there is provided for the first time (S) α-cyano-3-phenoxy-benzyl acetate free of its (R) form. There is also provided a novel process for the preparation of (S) α-cyano-3-phenoxy-benzyl acetate.
The novel product of the invention is (S) α-cyano-3-phenoxy-benzyl acetate of the formula: ##STR2## which has a positive specific rotation which is a value of about [α]D 20=+17.1° when measured at a concentration of 10% in benzene. The process of the invention for the preparation of (S) α-cyano-3-phenoxy-benzyl acetate comprises reacting (R,S) α-cyano-3-phenoxy-benzyl acetate with a lipase originating from a microorganism and capable of asymmetrically hydrolyzing the (R) α-cyano-3-phenoxy-benzyl acetate ester to give optically active (R) α-cyano-3-phenoxy-benzyl alcohol and (S) α-cyano-3-phenoxybenzyl acetate. The ester of the (S) alcohol and the (R) alcohol are then separated from the reaction mixture and thereafter the ester of the (S) alcohol is separated and recovered from the (R) alcohol.
The lipases employable in the present invention are those capable of asymmetrically hydrolyzing the ester of (R) α-cyano-3-phenoxy-benzyl alcohol and they are originated from microorganisms. One example of an employable lipase is a carboxylic acid hydrolase originated from the genus Candida, and particularly, the strain Candida cylindricae, also known as Candida rugosa. The enzyme is commercially available from the Sigma Chemical Company, Post Office Box 14508, St. Louis, Mo. 63178.
In practicing the process of the present invention, the asymmetric hydrolysis of the (R) ester is carried out by stirring or shaking a racemic mixture of (R,S) α-cyano-3-phenoxy-benzyl acetate and a lipase-containing liquor, such as a cultured liquor of such microorganism, its filtrate, lipase extracted liquor and its concentrate, a suspension of microorganism cells or aqueous solution containing crude or purified lipase preparation.
The process can be carried out at ambient conditions although it is preferred to carry out the reaction at elevated temperatures varying from about 40° C. to 50° C. since at elevated temperatures the reaction rates are much faster. The period of time for the reaction is typically from about 10 to 40 hours. However, the reaction time can be shortened by increasing the reaction temperature or by increasing the concentration of enzyme.
It is essential to control the pH of the reaction medium during the asymmetric hydrolysis reaction because α-cyano-3-phenoxy-benzyl alcohol tends to decompose when exposed to a basic substance. That is, exposure to a basic medium results in the decomposition of the alcohol although the hydrolysis reaction proceeds. Accordingly, the hydrolysis reaction should be conducted at a pH no higher than pH 8. Furthermore, a pH which is too low will cause deactivation of the enzyme. Thus, the reaction is preferably conducted in the range of pH 4 to pH 8, most preferably pH 5 to pH 6. A buffer solution may be used to prevent the lowering of the pH value due to the formation of organic acid during the course of hydrolysis. Either an inorganic or organic salt buffer can be used as the buffer solution.
After the asymmetric hydrolysis reaction, the (S) α-cyano-3-phenoxy-benzyl acetate ester and the (R) alcohol are separated from the reaction mixture by solvent extraction, liquid phase separation by standing, column chromatography or other conventional separation techniques. The ester is then separated from the alcohol by chromatography, preferably chromatography over silica gel.
Methods for producing the racemic mixture of (R,S) α-cyano-3-phenoxy-benzyl acetate from which the (S) α-cyano-3-phenoxy-benzyl acetate is obtained by the method of the present invention are known in the art. For example, an alkali metal cyanide, such as sodium cyanide, can be reacted with 3-phenoxybenzyldehyde and acetyl chloride in methylene chloride containing tetrabutylammonium bromide (Chem. Abstracts, 96(25):217504j) to produce the racemic mixture.
(S) α-cyano-3-phenoxy-benzyl acetate is useful as an intermediate for the production of synthetic pyrethroids such as fenvalerate, cypermethryn, and decamethrin and is deemed to possess insecticidal, herbicidal and bactericidal activities of its own.
The present invention is further described by means of the following examples. However, it is to be understood that the invention is not intended to be limited by these examples.
To 123 milliliters of 0.2M concentration of a sodium acetate buffer solution (pH 5.0) were added 30 grams of (R,S) α-cyano-3-phenoxy-benzyl acetate and 2.25 grams of Candida cylindricae lipase. The mixture was incubated with stirring at 50° C. for 23 hours. Samples were removed periodically and analyzed by gas chromatography. At the end of the 23-hour reaction period, it was determined that the mixture contained 53% α-cyano-3-phenoxy-benzyl alcohol and 47% α-cyano-3-phenoxy-benzyl acetate.
The reaction mixture was then extracted with toluene. The toluene extract was concentrated by vacuum distillation to yield a yellow oil. The yellow oil was mixed with 123 milliliters of 0.2M concentration of a sodium acetate buffer solution (pH 5.0) and 2.25grams of Candida cylindricae lipase. The mixture was incubated with stirring at 25° C. for 18 hours and extracted with toluene as described above to yield a yellow oil containing 37% α-cyano-3-phenoxy-benzyl acetate, 45% α-cyano-3-phenoxy-benzyl alcohol and 15% m-phenoxybenzaldehyde as determined by gas chromatography.
The oil was then extracted with 15 equal volumes petroleum ether (boiling point 35°-60° C.). These fractions were combined and concentrated by vacuum distillation to yield a yellow oil containing 67% α-cyano-3-phenoxy-benzyl acetate, 15% α-cyano-3-phenoxy-benzyl alcohol and 17% m-phenoxybenzaldehyde. This oil was analyzed on NMR using a chiral shift reagent [Eu(C12 H14 Fe3 O2)]. The analysis showed that the α-cyano-3-phenoxy-benzyl acetate consisted only of (S) α-cyano-3-phenoxybenzyl acetate.
The (S) α-cyano-3-phenoxy-benzyl acetate was purified by column chromatography. The oil was placed on a column containing Kieselgel 40 (60-230 mesh) and eluted with a mixture of heptane and ethyl acetate in a ratio of 85 parts heptane to 15 parts ethyl acetate. The fractions containing only (S) α-cyano-3-phenoxy-benzyl acetate were combined and concentrated by vacuum distillation to yield a yellow oil. The oil (116 milligrams) was combined with enough benzene to bring the total volume to 1.16 milliliters. The benzene solution was analyzed on a Perkin-Elmer Model 241 Polarimeter and yielded a positive rotation of +17.1° at 20° C.
To 886 milliliters of 0.2M concentration of a sodium acetate buffer solution (pH 5.0) were added 100 grams of (R,S)α-cyano-3-phenoxy-benzyl acetate and 6.0 grams of Candida cylindricae lipase. The mixture was incubated with rapid stirring at room temperature for 18 hours. With the cessation of stirring, the mixture separated into two phases. The lower, oily phase was collected and centrifuged to remove the enzyme. The protein was washed with toluene and the toluene fraction was added to the supernatant oil. The combined fractions were washed with NaCl saturated water and then dried over anhydrous magnesium sulfate. The toluene was removed by vacuum distillation to yield 68.9 grams of yellow oil.
The yellow oil was placed on a column containing Kieselgel 40 (60-230 mesh) and eluted with heptane:ethyl acetate (65:35). Fractions were collected and concentrated by vacuum distillation. Three fractions were obtained. These contained, respectively, 23.2 grams of α-cyano-3-phenoxy-benzyl acetate, 4.5 grams of α-cyano-3-phenoxy-benzyl alcohol, and a mixture of α-cyano-3-phenoxy-benzyl acetate and α-cyano-3-phenoxy-benzyl alcohol.
The α-cyano-3-phenoxy-benzyl acetate fraction was analyzed on NMR using a chiral shift reagent [Eu(C12 H14 F3 O2)3]. Analysis showed that the α-cyano-3-phenoxy-benzyl acetate consisted of a mixture containing 75-85% (S)α-cyano-3-phenoxy-benzyl acetate and 15-25% (R)α-cyano-3-phenoxy-benzyl acetate.
The α-cyano-3-phenoxy-benzyl alcohol fraction was analyzed by high performance liquid chromatography as described in Example 1. The α-cyano-3-phenoxy-benzyl alcohol fraction consisted exclusively of (R)α-cyano-3-phenoxy-benzyl alcohol.
Claims (5)
1. A method for biotechnologically preparing optically active (S) α-cyano-3-phenoxy-benzyl acetate which comprises reacting (R,S) α-cyano-3-phenoxy-benzyl acetate of the formula ##STR3## with a carboxylic acid hydrolase originating from a microorganism of the species Candida cylindriae and capable of asymmetrically hydrolyzing the ester of said formula to give optically active (S) α-cyano-3-phenoxy-benzyl acetate.
2. A method of claim 1 wherein said reaction is performed at a pH not higher than 8.
3. A method of claim 2 wherein said reaction is performed at a pH of from about 5 to about 6.
4. A method of claim 1 wherein said reaction is performed at a temperature of from about 40° C. to about 50° C.
5. A method of claim 1 wherein said reaction is performed at a pH of from about 5 to about 6, at a temperature of from about 40° C. to about 50° C., during a time of from about 10 to about 40 hours.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/226,824 US4897357A (en) | 1985-12-31 | 1988-08-01 | (S) α-cyano-3-phenoxy-benzyl acetate |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US06/815,207 US4827013A (en) | 1985-12-31 | 1985-12-31 | (S) α-(cyano-3-phenoxy-benzyl acetate |
US07/226,824 US4897357A (en) | 1985-12-31 | 1988-08-01 | (S) α-cyano-3-phenoxy-benzyl acetate |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/815,207 Division US4827013A (en) | 1985-12-31 | 1985-12-31 | (S) α-(cyano-3-phenoxy-benzyl acetate |
Publications (1)
Publication Number | Publication Date |
---|---|
US4897357A true US4897357A (en) | 1990-01-30 |
Family
ID=26920910
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US07/226,824 Expired - Fee Related US4897357A (en) | 1985-12-31 | 1988-08-01 | (S) α-cyano-3-phenoxy-benzyl acetate |
Country Status (1)
Country | Link |
---|---|
US (1) | US4897357A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1990015146A1 (en) * | 1989-06-05 | 1990-12-13 | Rhone-Poulenc Inc. | Enzymes and their use |
US4985365A (en) * | 1981-11-28 | 1991-01-15 | Sumitomo Chemical Company, Ltd. | Process for producing optically active benzyl alcohol compound |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0118163A1 (en) * | 1983-01-10 | 1984-09-12 | Sumitomo Chemical Company, Limited | Method for biotechnologically preparing optically active alpha-cyano-3-phenoxybenzyl alcohol |
JPS59220194A (en) * | 1983-05-27 | 1984-12-11 | Sumitomo Chem Co Ltd | Preparation of optically active ester |
US4601987A (en) * | 1985-02-27 | 1986-07-22 | Massachusetts Institute Of Technology | Enzymatic production of optical isomers of 2-halopropionic acids |
US4762793A (en) * | 1985-03-22 | 1988-08-09 | Montedison S.P.A. | Process for the biotechnological preparation of optically active alpha-arylalkanoic acids |
-
1988
- 1988-08-01 US US07/226,824 patent/US4897357A/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0118163A1 (en) * | 1983-01-10 | 1984-09-12 | Sumitomo Chemical Company, Limited | Method for biotechnologically preparing optically active alpha-cyano-3-phenoxybenzyl alcohol |
JPS59220194A (en) * | 1983-05-27 | 1984-12-11 | Sumitomo Chem Co Ltd | Preparation of optically active ester |
US4601987A (en) * | 1985-02-27 | 1986-07-22 | Massachusetts Institute Of Technology | Enzymatic production of optical isomers of 2-halopropionic acids |
US4762793A (en) * | 1985-03-22 | 1988-08-09 | Montedison S.P.A. | Process for the biotechnological preparation of optically active alpha-arylalkanoic acids |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4985365A (en) * | 1981-11-28 | 1991-01-15 | Sumitomo Chemical Company, Ltd. | Process for producing optically active benzyl alcohol compound |
WO1990015146A1 (en) * | 1989-06-05 | 1990-12-13 | Rhone-Poulenc Inc. | Enzymes and their use |
US5108916A (en) * | 1989-06-05 | 1992-04-28 | Rhone-Poulenc Rorer, S.A. | Process for stereoselectively hydrolyzing, transesterifying or esterifying with immobilized isozyme of lipase from candida rugosa |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0195717B1 (en) | Process for the biotechnological preparation of optically active alpha-arylalkanoic acids | |
CA1115699A (en) | Lithium pseudomonate and its preparation | |
DE3886445T2 (en) | Optically active compounds and processes for their production. | |
EP0127386B1 (en) | Process for producing optically active cyclopentenolones | |
US4897357A (en) | (S) α-cyano-3-phenoxy-benzyl acetate | |
US4827013A (en) | (S) α-(cyano-3-phenoxy-benzyl acetate | |
DE69221685T2 (en) | METHOD FOR PRODUCING OPTICALLY ACTIVE 3-CHLORINE-1-PHENYL-PROPAN-1-OL AND ITS DERIVATIVE | |
US4865771A (en) | Process for preparing L(-)-carnitine chloride from 3,4-epoxybutyric esters and novel intermediate compounds | |
JPH0155000B2 (en) | ||
EP0239122B1 (en) | Process for the enzymatic resolution of racemic 2-amino-1-alkanols | |
JPH0533995B2 (en) | ||
JPH01281098A (en) | Production of optically active carboxylic acid and optically active carboxylic acid ester | |
US5272069A (en) | Method of producing optically active hydroxyesters | |
JPH08119958A (en) | Production of optically active chroman compound | |
US5654440A (en) | Method for production of optically active (+)-4,4,4-trifluoro-3-(indole-3-)butyric acid | |
JPH0688947B2 (en) | Process for producing itaconic acid 1-monoester | |
JPS5953838B2 (en) | Method for producing β-hydroxyvaleric acid | |
JPS6012992A (en) | Production of optically active carboxylic acid | |
JPH0728754B2 (en) | Biochemical production method of optically active 4-hydroxycyclopentenones | |
JP2538231B2 (en) | Process for producing optically active 4-pentene-2-ol derivative | |
JPH04228093A (en) | Production of optically active alpha-hydroxyalkenoic acid derivative | |
JPS5953839B2 (en) | Method for producing (−)-α-hydroxymethylbutyric acid | |
JPH0679558B2 (en) | Biochemical production method of (R) -4-hydroxy-2-cyclopentenone | |
JPS6012993A (en) | Production of optically active carboxylic acid | |
JPH07213295A (en) | Method for producing 4-hydroxy-2-methylbenzoic acid with microorganism |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Lapse for failure to pay maintenance fees | ||
FP | Lapsed due to failure to pay maintenance fee |
Effective date: 19930130 |
|
STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |